CN1329604A - A process for islation of 10-deacetyl baccatin III from recoverably part of plant of i(TAXUS) species - Google Patents
A process for islation of 10-deacetyl baccatin III from recoverably part of plant of i(TAXUS) species Download PDFInfo
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- CN1329604A CN1329604A CN99814181A CN99814181A CN1329604A CN 1329604 A CN1329604 A CN 1329604A CN 99814181 A CN99814181 A CN 99814181A CN 99814181 A CN99814181 A CN 99814181A CN 1329604 A CN1329604 A CN 1329604A
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- C07D305/00—Heterocyclic compounds containing four-membered rings having one oxygen atom as the only ring hetero atoms
- C07D305/14—Heterocyclic compounds containing four-membered rings having one oxygen atom as the only ring hetero atoms condensed with carbocyclic rings or ring systems
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- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K2236/00—Isolation or extraction methods of medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicine
- A61K2236/30—Extraction of the material
- A61K2236/33—Extraction of the material involving extraction with hydrophilic solvents, e.g. lower alcohols, esters or ketones
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K2236/00—Isolation or extraction methods of medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicine
- A61K2236/50—Methods involving additional extraction steps
- A61K2236/53—Liquid-solid separation, e.g. centrifugation, sedimentation or crystallization
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Abstract
A novel process for isolation of 10-deacetyl baccatin-III (10-DAB) and also complete separation of paclitaxel present in the primary extract, on a commercial scale from plant extract of Taxus species by solvent crystallization without employing chromatographic separation.
Description
The technical field of the invention
This invention relates to field of phytochemistry.Or rather, it provides a kind of simple and economic method, is used for extracting from the leaf tissue of european yew (Taxus baccata) 10-deacetylation baccatin III (being called for short 10-DAB) composition.10-DAB is used to prepare the main chain intermediate that taxol, many West Platforms restrain this (docetaxel) and analogue thereof.
The application is the part continuity of No. the 09/212nd, 321, the United States Patent (USP) of 15 days December in 1998 registration formerly.Patent application formerly (No.09/212,321) is described the leaching process of 14 beta-hydroxy 10-deacetylation baccatin III.
Background of invention
10-deacetylation baccatin III (10-DAB) is the very important precursor that taxol biosynthesis and many West Platforms restrain this (docetaxel) analogue.Taxol (paclitaxel) and many West Platforms restrain this (docetaxel) analogue to have outstanding cytotoxicity and [sees " pharmaceutical chemistry magazine " (J.Med.Chem.) .1977 in the clone of human ovarian cancer, lung cancer, colorectal carcinoma and mammary cancer of opposing, 40,267-278].
10-deacetylation baccatin III (10-DAB) adopts following structural to express:
(p1 figure)
Have been found that at present compound 10-deacetylation baccatin III is the highest in the concentration of the trunk of Ramulus et folium taxi cuspidatae class plant (Taxus) and blade-section, but this composition is also contained at other position of plant, just concentration is relatively low.
The method of the most common separation 10-DAB comprises and adopts alcohols or any protonic solvent to extract biomaterial, produces extracting solution through half purification of the distribution/steeping process of solvent, and last with optionally crystallization or chromatography method prepare 10-DAB.Here provide the method for some common extraction 10-DAB:
United States Patent (USP) has been described about extracting biomaterial with fatty alcohol for No. 5393895, subsequently dilute with water and isolate the process of insoluble substance.Remove all alcohols materials then, keep the aqueous solution, this part distributes with organic solvent again, produces 10-DAB at last through crystallisation process optionally.
United States Patent (USP) is for No. 5736366 about obtaining the process of 10-deacetylation baccatin III.This process comprises uses the water extraction biomaterial, adsorbs with a kind of suitable dielectric material then, carries out desorb with a kind of organic solvent again, obtains 10-DAB with crystallization method optionally at last.
United States Patent (USP) is for No. 5453521 with fatty alcohol solution-treated biomaterial, dilute with water separates undissolved material and aquation alcoholic solution then, removes alcohols subsequently fully, use the organic solvent extraction aqueous solution again, adopt the selective crystallization method to obtain 10-DAB at last.
United States Patent (USP) is to use the water treatment biomaterial No. 5393896, handles water-phase extract with organic solvent then, further adopts optionally crystallization method to produce 10-DAB again to organic phase part.
WO94/07881 uses the water extraction biomaterial, it is adsorbed on a kind of suitable dielectric material then, or does not adsorb, and handles with organic solvent subsequently, obtains 10-DAB with the selective crystallization method again.
WO94/07882 extracts biomaterial with methyl alcohol, and dilute with water is removed insolubles then.Subsequently the alcohols material of soluble part is separated fully, obtained the aqueous solution, this part solution distributes with appropriate organic solvent again, and then obtains 10-DAB with the selective crystallization method.
Above-mentioned all formerly all do not relate to the taxol (paclitaxel) that how will be present in the biomaterial in the processing method and separate, and taxol is the medicine of a kind of very important treatment ovarian cancer and mammary cancer.Said process is not separated taxol fully from 10-DAB in addition, and it remains in the primary extract.In addition, in existing method of separating 10-DAB from Ramulus et folium taxi cuspidatae class plant (Taxus), the method for the present invention's narration is the most economical and to eco-friendly.
Goal of the invention
Therefore, one of purpose of the present invention provides a kind of simple, economic method and separates 10-DAB (10-deacetylation baccatin III), and this compound can be used as the analogue intermediate that taxol biosynthesis and many West Platforms restrain this (docetaxel).
Another object of the present invention provides and adopt this dull separating step of chromatographic technique a kind of not comprising in each step of separating 10-DAB.
And a further object of the invention is, the solvent that is adopted in whole sepn process different step can recycle.
In addition, the present invention also provides the novel method that can extract 10-DAB from arbitrary position of various Ramulus et folium taxi cuspidatae class plants (Taxus).
One of purpose of the present invention also is to provide complete isolated taxol method from the primary extract that contains 10-DAB, therefore need not just can obtain this two kinds of materials through trivial step.
According to above-mentioned purpose with other, the invention provides a kind of novel method that can in commercial production, use, be used for extracting 10-deacetylation baccatin III (10-DAB), and from primary extract isolation of taxol fully.This method is to adopt solvent crystallization and need not to extract 10-deacetylation baccatin III and taxol through the method for chromatographic separation from Ramulus et folium taxi cuspidatae class plant (Taxus).Detailed Description Of The Invention
The invention provides a kind of novel method, be used for separating 10-deacetylation baccatin III (10-DAB), this compound can be used for taxol biosynthesis and many West Platforms and restrain the analogue of this (docetaxel) etc.
Narrated a kind of novel method that can be for commercial applications, can from Ramulus et folium taxi cuspidatae class plant (Taxus) tissue, extract 10-deacetylation baccatin III (10-DAB), and can be from primary extract isolation of taxol fully.Described method comprises following steps: prepare the alcohols extract of the dry blade of Ramulus et folium taxi cuspidatae class plant (Taxus), handle with aliphatic ketone subsequently, then with mother liquid evaporation, obtain some residues; Handle with the solvent mixture of the ketone aqueous solution again, separate insoluble component after, with the organic solvent extraction ketone aqueous solution, separate 10-DAB with crystallization method optionally at last.
Whole process is very simple, and 10-deacetylation baccatin III (10-DAB) can separate selectively with the renewable tissue part of crystalline method from Ramulus et folium taxi cuspidatae class plant (Taxus).Its process may further comprise the steps:
(a) material of the Ramulus et folium taxi cuspidatae class plant (Taxus) that will pulverize, also can dry as required extracts with fatty alcohol,
(b) the alcohols extract that contains 10-DAB is carried out partial concentration,
(c) handle the said extracted thing with aliphatic ketone, and insolubles separated from mother liquor with centrifugal or filtering method,
(d) with behind the resulting mother liquid evaporation of step c, obtain a kind of residue; Handle residue obtained with the miscellany of aliphatic ketone and water again.Adopt method by bed of diatomaceous earth to filter then or centrifugally remove insoluble material, it is rich in taxol.
(e) solution after aliphatic ketone extracts does not contain taxol fully, remove coloring matter with aromatic hydrocarbon after, extract with aliphatic ester or chlorinated hydrocarbon solvent again,
(f) organic phase of step e is evaporated near doing, obtains semisolid residue thing, promptly obtain 10-DAB after to its processing with crystallization method optionally,
(g) separate also purifying 10-DAB
The insolubles that obtains after adopting the miscellany of aliphatic ketone and water to handle in step (d) has the advantage of can be fully 10-DAB and the taxol that is present in the elementary alcohols extract being separated.After insolubles separately carried out independent purifying, can purification of paclitaxel.Therefore, said process can separate with 10-DAB taxol from natural product.
In addition, use the particularly advantageous part of acetone to be in step (c) in this technology, can be used for separating 10-DAB and taxol from the elementary alcohols extract that contains low ratio impurity.
In one embodiment, the fatty alcohol that is used to prepare the alcohols extract is selected from methyl alcohol, ethanol, propyl alcohol, Virahol, the trimethyl carbinol.
What one of feature was that fatty alcohol adopts is methyl alcohol.
In another embodiment, be immersed in the powder at Ramulus et folium taxi cuspidatae class plant (Taxus) position of any oven dry in methyl alcohol, ethanol, propyl alcohol, Virahol or the trimethyl carbinol kind solvent, can obtain the alcohols extract by continuous stirring.
Another feature of invention, be to adopt the fatty nitrile solvent at random to mix with the fatty alcohol that is selected from methyl alcohol, Virahol, the trimethyl carbinol, perhaps mix, handle the crystallization that residue obtains 10-DAB then with the aliphatic ester that is selected from ethyl acetic ester, propionyl acetic ester and isoamyl acetic ester.Fatty nitrile is selected from acetonitrile and propionitrile.
Another feature is that 10-DAB extracts from any kind any part of Chinese yew genus plants (Taxus).
Another feature is that 10-DAB carries out centrifugation to come out after the crystallization.Another feature is that the position of plant is a blade.
Another feature is that taxol separates with the two and the 10-DAB that deposits in primary extract fully.
The process of above-mentioned extraction 10-DAB is not included in any chromatographic technique in any stage.Preferred technology may further comprise the steps:
1. Ramulus et folium taxi cuspidatae class plant (Taxus) must be through pulverizing, and can further dry as required.From methyl alcohol, ethanol, propyl alcohol, Virahol, the trimethyl carbinol, select water miscible fatty alcohol to add in the blade powder, miscellany was stirred 12 hours.Used fatty alcohol methyl alcohol preferably in this process.
2. resulting half concentrates alcohol extract contains 10-DAB, taxol and other taxines material (TAXANES).Described extract and aliphatic ketone are mixed to be stirred 1 hour.Centrifugation is filtered or used to insoluble then component with bed of diatomaceous earth.Remaining liquid is the mother liquor that the back can further process.
3. obtain resistates behind the mother liquor of vaporising under vacuum in the 2nd step, water and ketone mix solvent treatment again, filter or insoluble part is filtered with bed of diatomaceous earth or centrifugal with the method for centrifugation with bed of diatomaceous earth, obtain being rich in the material of taxol, further again processing just obtains taxol.The resulting clarifying ketone aqueous solution can be used for further processing and isolates 10-DAB.
4. the resulting clarifying ketone aqueous solution does not conform to taxol fully, removes the small amount of polar material with arene compound, and that remaining is 10-DAB.Then, the remaining water-soluble liquid phase water-immiscible solvent of ketone, preferably aliphatic ester or chloro kind solvent extract 10-DAB fully.
5. after this, the extract of organic solvent under vacuum 80 ℃-90 ℃ be evaporated to drying and obtain semisolid resistates.Subsequently, use fatty nitrile solution in the resistates that thick 10-DAB obtains from above again, obtain crystallization selectively as acetonitrile, propionitrile arbitrarily and fatty alcohol such as methyl alcohol, Virahol, the trimethyl carbinol or handle, with the mixture of aliphatic ester such as acetone, ethylhexoate, butylacetic acid ester.Optionally crystallization more has superiority in acetonitrile, perhaps at ethanol, methyl alcohol or ethyl acetate and/or butylacetate.Can adopt purifying 10-DAB such as centrifugal after any traditional method such as the crystallization.
The novel method of above-mentioned separation 10-DAB can be used for extracting from any part of Ramulus et folium taxi cuspidatae class plant (Taxus.sp.), as european yew (T.baccata), yewtree (T.brevifolia), T. canadensis (T.cannadensis), taxus chinensis in northeast (T.cuspidata), Florida Ramulus et folium taxi cuspidatae (T.flodridara), hybrid Japanese yew (T.media), Xizang Taxus chinensis (T.wallichiang).Technology of the present invention is simple, and does not comprise chromatography method in any stage of process, only just can obtain with solvent.
Another advantage of this method is that solvent used in different step is all recycling.In addition, the applicant finds, although contain 10-DAB and taxol in the starting material of usefulness in the present invention, successfully isolation of taxol is in order to commercial production for the latter, and this innovation is not obtain in the former invention.
The method of above-mentioned novelty can describe in detail with the following example, and these embodiment just are used for explanation and are not intended to go to limit scope of the present invention.
Example I
The leaf of european yew (Taxus baccata) is ground, can select further oven dry.The size of blade powder should be near the 0.6-0.8 millimeter.(15-45 ℃) at ambient temperature, the 1000 liters of methyl alcohol of leaf adding to 100 kilograms of grindings stirred (per minute 58 changes) 12 hours, carried out alcohols and extracted.The methanol solution that obtains after centrifugal reduces pressure in evaporating pot (150m bar), evaporate under the 40-50 ℃ condition, obtains half enriched material, and its weight approximately is the 20-30% of leaf weight.
To at room temperature mix with 25 kilograms half concentrated methanol extract (containing 0.12% 10-DAB, 20% water and 10% methyl alcohol) of method for preparing, stirred 1-2 hour with 175 liters of acetone.The insolubles that occurs is with filtering or the centrifugation method separation.Acetone solution thing in the mother liquor accounts for half and concentrates 35% of extract weight, it is leached, in vacuum condition (150m bar) and 40-50 ℃ of following drying.
Add 43.75 liters of acetone and softening water (DM) mixed solution (ratio 2: 8) in resulting 8.75 kilograms of residues, (per minute 72 changes) stir about is 2 hours at room temperature at a high speed.Filter or centrifugally remove insoluble material with bed of diatomaceous earth.Owing to be rich in taxol in the insoluble material, but therefore by isolating the taxol of commercial applications after the further processing.The ketone aqueous solution mother liquor of collecting is clarification, garnet.
Do not contain taxol in the ketone aqueous layer fully, divide 2 times with 17.5 liters of toluene, extract by stirring (per minute 40 changes) with 8.75 liters at every turn, the each extraction stirred 1 hour.
Behind methylbenzene extraction, resulting moisture ketone layer at room temperature (15-45 ℃) extracts with methylene dichloride (4 * 16.5 liters), extracts 30 minutes under the condition that per minute 40 changes at every turn.Dichloromethane extract is merged the back use dried over sodium sulfate, (150m bar) carries out drying in 25-65 ℃ in vacuum flask under vacuum condition then.The methylene dichloride resistates generally accounts for the 1.5-1.8% of half spissated methanol extract weight, contains the 10-DAB of 4.5-6%.
Example II
Under the preparation condition of example I, the dry extract of 468.7 grams contains 5.1% 10-DAB.Extract changes with per minute 40 50-60 ℃ the time with 975 milliliters acetonitrile and stirs.After extract dissolves fully, mixture was cooled off 12-16 hour down at 0-5 ℃, stirring under (per minute 20 changes) condition at a slow speed then.Insoluble solids is used 50 milliliters acetonitrile drip washing again with filtering or the centrifugation method separation.Under decompression (0.5mbar) and 60-70 ℃, dry 12 hours, obtain 29.43 and restrain solids, it contains 76.1% 10-DAB.EXAMPLE III
Will be under the example II condition resulting 29.43 gram solids 70 ℃ reflux down and stir (per minute 58 changes) 1 hour, are dissolved in 735.5 milliliters the methyl alcohol.Gained solution is cooled to room temperature (15-45 ℃), filters with bed of diatomaceous earth then and obtains clear liquid.Filtrate is stirred down in slow condition (per minute 20 change), simultaneously 295 milliliters acetonitrile is added lentamente.Mixture is cooled to 0-5 ℃, and keeps 12-15 hour.To precipitate with filtering or centrifugal method separates, carry out wash-out with the mixed solution of 10 milliliters methyl alcohol and acetonitrile (ratio 1: 1).With the elutriant that obtains individual hour of dry 20-30 under decompression (0.5m bar) and 90-95 ℃ of condition.Obtain the white mass of 22.2 grams at last, contain 94.1% 10-DAB.
The mother liquor revaporization that obtains after the last crystallization is extremely done the purifying 10-DAB that is used for capable of circulation.
EXAMPLE IV
The thick product solid of 30 grams that obtains in the example II with 750 milliliters of acetone under 65 ℃ of conditions backflow 1-2 hour, is dissolved.Solution is cooled to room temperature, filters with bed of diatomaceous earth then.Filtrate is stirred under low speed (20rmp) condition, simultaneously the 200ml acetonitrile is slowly added.The temperature of solution is dropped to 0-5 ℃, kept 15-20 hour.Use the centrifugal method precipitation separation, and carry out wash-out with the mixed solution of acetone and acetonitrile (ratio 1: 1).Last product under decompression (0.5m bar) and 80-90 ℃ of condition dry 12-20 hour, the product that obtains at last (23.1 restrain) contains 93.5% 10-DAB.The advantage of novel process: a) simple, economical, the commercialization advantage arranged.B) any stage in the described process of present method does not comprise loaded down with trivial details chromatographic technique.C) employed solvent can recycle in the many steps in present method.D) present method is applicable to any part e that extracts different sorts Ramulus et folium taxi cuspidatae class plant (Taxus)) present method can be used for separating the natural Japanese yew alkylol cpd that is present in the elementary alcohols extract.F) according to raw-material quality characteristic, the quantum of output of 10-DAB should account for the 60-90% of starting material content.
Claims (11)
1. the technology of separating 10-DAB from the renewable part of different Ramulus et folium taxi cuspidatae class plants with crystallization method comprises the steps:
(a) will grind, and the part of drying Ramulus et folium taxi cuspidatae class plant (Taxus) as required extract with fatty alcohol;
(b) carry out partial concentration to containing the elementary alcohols extract of 10-DAB;
(c) handle extract with aliphatic ketone, insoluble substance is separated from mother liquor with centrifugal or filtering method;
(d) mother liquor to step (c) carries out reduction vaporization under vacuum condition, obtain residual substance, handle this resistates with the mixed solvent of aliphatic ketone and water, filter or centrifugally remove insoluble material with bed of diatomaceous earth, this material is rich in taxol, can obtain the taxol of commercial standards by further processing;
(e) isolated aliphatic ketone extracting solution does not contain taxol fully, removes the low-pole material with aromatic hydrocarbon, extracts with water-fast aliphatic ester or chlorinated hydrocarbon solvent again;
(f) organic phase of evaporation step (e) is done near, obtains semisolid resistates, therefrom promptly obtains 10-DAB through crystallization optionally; And
(g) separate also purifying 10-DAB.
2. technology according to claim 1, the wherein said fatty alcohol that is used to prepare the alcohols extract is selected from methyl alcohol, ethanol, propyl alcohol, Virahol, the trimethyl carbinol.
3. technology according to claim 1, wherein said fatty alcohol is a methyl alcohol.
4. technology according to claim 1, wherein said alcohols extract are to obtain by the different sites that ground, that also can carry out exsiccant Ramulus et folium taxi cuspidatae class plant (Taxus sp) that stirring is immersed in methyl alcohol, ethanol, propyl alcohol, Virahol, the trimethyl carbinol.
5. in the method according to claim 1, wherein said 10-DAB carries out selective crystallization, be with fatty nitrile solution arbitrarily with different fatty alcohol mixing, handle that semisolid residue obtains.
6. method according to claim 1, wherein said fatty nitrile solution is selected from acetonitrile and propionitrile.
7. method according to claim 1, wherein said fatty nitrile solution or mix with the fatty alcohol that is selected from methyl alcohol, Virahol, the trimethyl carbinol perhaps mixes with the aliphatic ester that is selected from ethyl acetate, propionyl acetate and isoamyl acetate.
8. method according to claim 1, wherein said 10-DAB extracts from any part of any kind of of Taxus (Taxus).
9. method according to claim 1, wherein said 10-DAB be carry out centrifugal after the crystallization or filter after separate.
10. method according to claim 1, wherein said plant are european yew (Taxus baccata).
11. method according to claim 1, wherein said plant part is a leaf.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/212,321 US6002024A (en) | 1998-07-27 | 1998-12-15 | Process for the isolation of 14β-hydroxy-10-deacetyl baccatin-III |
| US09/212,321 | 1998-12-15 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1329604A true CN1329604A (en) | 2002-01-02 |
| CN1150179C CN1150179C (en) | 2004-05-19 |
Family
ID=22790517
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB99814181XA Expired - Fee Related CN1150179C (en) | 1998-12-15 | 1999-09-07 | A process for islation of 10-deacetyl baccatin III from recoverably part of plant of i(TAXUS) species |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US6002024A (en) |
| EP (1) | EP1010697B1 (en) |
| JP (1) | JP4435988B2 (en) |
| KR (1) | KR100561111B1 (en) |
| CN (1) | CN1150179C (en) |
| AT (1) | ATE207912T1 (en) |
| AU (1) | AU753086B2 (en) |
| BR (1) | BR9916805A (en) |
| CA (1) | CA2354847C (en) |
| DE (1) | DE69900406T2 (en) |
| ES (1) | ES2167999T3 (en) |
| WO (1) | WO2000035896A1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105085443A (en) * | 2015-09-21 | 2015-11-25 | 四川农业大学 | Method for using Taxus media branches and leaves as raw material to prepare high-purity 10-deacetyl baccatin III |
| CN102827106B (en) * | 2012-08-29 | 2017-11-07 | 宁波绿之健药业有限公司 | A kind of 10-DAB method for extraction and purification |
| CN110882213A (en) * | 2019-11-21 | 2020-03-17 | 海南紫杉园制药有限公司 | Paclitaxel injection and preparation method thereof |
| CN113149935A (en) * | 2021-04-25 | 2021-07-23 | 迪庆顺源生物有限公司 | Extraction, separation and purification method of 10-DAB |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6124482A (en) * | 1998-07-27 | 2000-09-26 | Dabur Research Foundation | Process for isolation of 10-deacetyl baccatin-III |
| US6002024A (en) * | 1998-07-27 | 1999-12-14 | Dabur Research Foundation | Process for the isolation of 14β-hydroxy-10-deacetyl baccatin-III |
| US20030157208A1 (en) * | 2001-12-20 | 2003-08-21 | Rui Wang | Cynomoriaceae extract and use in treating erectile dysfunction |
| CN100404520C (en) * | 2006-08-15 | 2008-07-23 | 北京诺瑞医药技术有限公司 | Method of extracting and separating 10-deacetyl bakadin III from European yew branches and leaves |
| CN103145652B (en) * | 2013-03-05 | 2015-09-30 | 无锡尔云科技有限公司 | A kind of method extracting taxol and derivative thereof from Chinese yew genus plants |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1254517B (en) * | 1992-03-06 | 1995-09-25 | Indena Spa | 14-BETA IDROSSI-10-DEACETIL-BACCATINA III, ITS DERIVATIVES, THEIR PREPATION AND THERAPEUTIC USE |
| FR2696463B1 (en) * | 1992-10-05 | 1994-11-25 | Rhone Poulenc Rorer Sa | Process for obtaining 10-deacetyl baccatin III. |
| FR2714053B1 (en) * | 1993-12-22 | 1996-03-08 | Pf Medicament | Process for the extraction and isolation of 10-deacetylbaccatin III. |
| US6002024A (en) * | 1998-07-27 | 1999-12-14 | Dabur Research Foundation | Process for the isolation of 14β-hydroxy-10-deacetyl baccatin-III |
-
1998
- 1998-12-15 US US09/212,321 patent/US6002024A/en not_active Expired - Fee Related
-
1999
- 1999-08-05 ES ES99890261T patent/ES2167999T3/en not_active Expired - Lifetime
- 1999-08-05 EP EP99890261A patent/EP1010697B1/en not_active Expired - Lifetime
- 1999-08-05 AT AT99890261T patent/ATE207912T1/en not_active IP Right Cessation
- 1999-08-05 DE DE69900406T patent/DE69900406T2/en not_active Expired - Fee Related
- 1999-09-07 AU AU20000/00A patent/AU753086B2/en not_active Ceased
- 1999-09-07 CN CNB99814181XA patent/CN1150179C/en not_active Expired - Fee Related
- 1999-09-07 CA CA002354847A patent/CA2354847C/en not_active Expired - Fee Related
- 1999-09-07 BR BR9916805-7A patent/BR9916805A/en not_active IP Right Cessation
- 1999-09-07 KR KR1020017007366A patent/KR100561111B1/en not_active IP Right Cessation
- 1999-09-07 JP JP2000588157A patent/JP4435988B2/en not_active Expired - Fee Related
- 1999-09-07 WO PCT/IN1999/000041 patent/WO2000035896A1/en active IP Right Grant
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102827106B (en) * | 2012-08-29 | 2017-11-07 | 宁波绿之健药业有限公司 | A kind of 10-DAB method for extraction and purification |
| CN105085443A (en) * | 2015-09-21 | 2015-11-25 | 四川农业大学 | Method for using Taxus media branches and leaves as raw material to prepare high-purity 10-deacetyl baccatin III |
| CN110882213A (en) * | 2019-11-21 | 2020-03-17 | 海南紫杉园制药有限公司 | Paclitaxel injection and preparation method thereof |
| CN110882213B (en) * | 2019-11-21 | 2021-05-04 | 海南紫杉园制药有限公司 | Paclitaxel injection and preparation method thereof |
| CN113149935A (en) * | 2021-04-25 | 2021-07-23 | 迪庆顺源生物有限公司 | Extraction, separation and purification method of 10-DAB |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4435988B2 (en) | 2010-03-24 |
| JP2002532485A (en) | 2002-10-02 |
| DE69900406D1 (en) | 2001-12-06 |
| CA2354847A1 (en) | 2000-06-22 |
| DE69900406T2 (en) | 2002-07-11 |
| BR9916805A (en) | 2001-10-23 |
| EP1010697B1 (en) | 2001-10-31 |
| AU753086B2 (en) | 2002-10-10 |
| CA2354847C (en) | 2006-07-11 |
| WO2000035896A1 (en) | 2000-06-22 |
| AU2000000A (en) | 2000-07-03 |
| ATE207912T1 (en) | 2001-11-15 |
| KR20010093159A (en) | 2001-10-27 |
| EP1010697A3 (en) | 2000-07-19 |
| US6002024A (en) | 1999-12-14 |
| KR100561111B1 (en) | 2006-03-15 |
| CN1150179C (en) | 2004-05-19 |
| ES2167999T3 (en) | 2002-05-16 |
| EP1010697A2 (en) | 2000-06-21 |
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